Microbial fuel cell aerator

ABSTRACT

A device for mixing and aerating a body of water, the device includes a microbial fuel cell comprising an anode and a cathode; an electricity management subsystem electrically connecting the anode and the cathode; and a mixing subsystem electrically connected to the electricity management subsystem. The device can be used to mix or aerate a body of water containing organic material while simultaneously reducing the requirements for aeration. The body of water may provide organic material to the microbial fuel cell to produce electricity to power the mixing subsystem.

CROSS-REFERENCE TO RELATED APPLICATION(S)

This application is a continuation of U.S. patent application Ser. No.13/557,006, filed Jul. 24, 2012, which claims priority to and thebenefit of Provisional Application No. 61/511,506, filed Jul. 25, 2011,entitled “MICROBIAL FUEL CELL AERATOR”, the entire content of both ofwhich is incorporated herein by reference.

FIELD

The present invention relates to a device to improve the mixing andaeration of industrial, agricultural and waste treatment ponds. Inparticular, the device relates to a microbial fuel cell configured toproduce energy to power a mixer or aerator with a synergistic feedbackto the biological oxygen demand of the water body.

BACKGROUND

Aeration, the process of purposely exchanging gases between theatmosphere and water, is a required aspect of many different biological,engineering and social systems. Most commonly, aeration is required toeither add a gas to water when its absence compromises a desired outcomeor removing a gas from water when its surplus is similarly unwanted. Inboth cases, engineers have created a wide variety of technologies toaccomplish these tasks. Most involve physical manipulations of thephysics of air-water gas exchange to enhance the exchange rate as wellas clever innovations to increase the effectiveness or reduce the costs.Some of these approaches also directly influence the need for aeration.

Although the dynamics of many different gases can require enhanced ratesof air-water gas exchange, one common application is the requirement foroxygen in waters that must support life. Photosynthesis, the basis ofnearly all life on earth, uses sunlight energy to create the chemicalbonds in organic material. Whether on land or in water, photosyntheticorganisms transform carbon dioxide into organic material and use wateras a source of electrons, thus making gaseous oxygen as a by-product ofthe water-splitting reaction. Animals and bacteria, commonly calledheterotrophic organisms, use this organic material as a source of energyfor their metabolism. In the process, they excrete carbon dioxide. Theyalso must find a terminal electron acceptor for the electron transportchain in respiration. Many organisms use oxygen for this purpose,thereby re-creating pure water, while some micro-organisms can use avariety of metals as the terminal electron acceptor.

The balance of oxygen production and oxygen respiration in any ecosystemdetermines the net changes in the constituents that are involved in theprocesses. Excess photosynthesis over respiration can lead to a buildupof organic material and oxygen and a decline in carbon dioxide andnutrients. Systems that have inputs of large amounts of exogenousorganic material can support the growth of stable populations oforganisms, but the oxygen content, or that of any other electronacceptors, will steadily decline. The state of any system will be afunction of these kinds of balances over any specific time and spacescale.

For example, sewage treatment plants bring in large amounts of organicwaste from urban environments with water as the carrier and break thatwaste down to inorganic nutrients as part of making the water safer fordischarge back into the environment. This is usually done by growingmicro-organisms on the organic waste to reduce the “Biological OxygenDemand” (“BOD”). BOD is a short-hand measure for how much oxygen wouldbe required to allow these organisms to aerobically metabolize all ofthe organic wastes to inorganic nutrients. Since these systems have anexogenous supply of organics, they generally require an exogenous sourceof oxygen. Typically, this is supplied by adding oxygen directly to thewater carrying the organic waste, either through enhanced gas exchangewith the oxygen in the atmosphere or through direct injection of pureoxygen.

Other managed water bodies have a related dynamic. Fish farms have alarge organic loading through the feed that is added to the ponds tosupport the growth and metabolism of the fish. Both unused feed and fishwastes stimulate the growth of bacteria and other micro-organisms.Similarly, many man-made bodies of water have large organic loadings,including the ponds at golf-courses, small fishing lakes near farms,harbors, waste ponds near agricultural food processing plants and manyothers. All of these have a similar issue. The pond may become anoxic ifthe oxygen drops too low, which may bring negative consequences. In thefish ponds or lakes, the fish and other large animals will die. In someof these, the anoxic ponds release noxious and foul smelling gases thatmake them an eyesore and nuisance.

Natural bodies of water also show similar dynamics. When organicloadings are high, the scenarios are similar to the fish ponds. However,natural bodies also can have unfortunate responses to the addition ofinorganic nutrients from either natural sources, for example upwelling,or manmade, for example nutrient discharge. In these cases, largepopulations of plants and algae will grow in a process calledeutrophication. As these populations of plants use up the nutrients, theorganic biomass sinks out and is subsequently consumed. While the plantsare growing near the surface, they make extra oxygen which outgases tothe atmosphere. As the organic material decays, it consumes oxygen untilthe dissolved oxygen is gone and the system becomes anaerobic. This canlead to dead-zones and other harmful ecosystem effects. These also tendto occur on spatial scales that are much too large for an effectiveengineering response after the organic material is present. Sometimeshumans can influence the original source of inorganic nutrients, such asremoving phosphates from detergents or reducing nutrient runoff fromfarms. However, sometimes eutrophication cannot be avoided.

While these examples are primarily centered on oxygen balance issues,there are other instances when enhanced gas exchange can be required.Large amounts of respiration will raise the amount of carbon dioxide inthe water and its removal can be advantageous in some cases. Conversely,growing algae or other aquatic plants actually requires carbon dioxideas a nutrient and it must be added if the rate of growth exceeds theability of the ecosystem to supply it naturally,

In most cases where there is too little oxygen, or too little or toomuch of any other gas, it is because the internal dynamics of the waterexceed the natural rate of gas exchange between water and air. Thetypical response is to increase the rate of gas exchange through one ofa variety of methods. Gas exchange rate is governed by a complex set ofphysical and chemical processes that are fairly well known. In general,the rate is a function of the surface area of the air-water interface,the concentration difference of the gases at the surface as indicated bytheir partial pressures and the mixing of water and air away from thissurface to homogenize with the concentrations in the wider body ofwater.

Enhancements to gas exchange rate generally involve a wide variety oftechnologies and engineered solutions that increase the concentrationgradient, increase the surface area and increase the turbulent mixingaway from the interface. The simplest of these involve some combinationof splashing and bubbling. Splashing puts drops of water into the air,increasing the effective amount of surface area and mixing the dropswith the wider body of water on impact. Bubbling puts small bubbles inthe water, again increasing surface area and, since bubbles rise, aidingin mixing. In both cases, increasing the gradient can be done either bycareful choice of timing and location for the splashing/bubbling toensure that the concentrations in the water and air are as different aspossible, for example drawing water from the bottom of a pond or atnight when the oxygen is lowest, or by using gas mixtures that have ahigher content of the gas of interest, for example pure oxygen or CO2.

These traditional aeration techniques are generally effective. However,they are also quite expensive in terms of their energy requirements.Physical methods generally require a lot of energy to move water andair. This energy is typically supplied by electricity produced by thecombustion of fossil fuels, whose volatile prices are ever increasing.Making pure gas mixtures is even more expensive. Thus, as fossil fueland energy prices rise and as the world discusses the consequences ofthe emission of fossil fuel carbon dioxide, the price component ofaeration begins to take a significant role in understanding thesustainability of various human practices. Technologies that can reducethese costs should have a positive impact on many human activities andbusinesses at the same time as they have a positive effect on theplanet.

SUMMARY

The invention relates to a microbial fuel cell aerator (“MFCA”), adevice for providing low-cost, low-carbon-emission aeration toorganic-rich waters. The MFCA takes advantage of the uniquecharacteristics of a microbial fuel cell (“MFC”) for providing renewablepower through waste treatment and adapts the MFC to also reduce theoxygen demand of a pond. The energy provided by the MFC is then used topower the desired aeration or mixing method, including, but not limitedto, traditional splashing or bubbling mechanisms. The combination ofthese approaches reduces the fossil-fuel electricity requirements foraeration to reduce the carbon emission, reduces the amount of aerationthat must be done and reduces the installation costs of the system.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a generic flow diagram for a microbial fuel cell showing theprocess of converting organic matter to electricity.

FIG. 2 is a schematic view of a floating microbial fuel cell aerator inaccordance with an embodiment of the invention.

FIG. 3 is a flowchart showing the process that can be used to convertorganic matter to electricity with the microbial fuel cell aerator ofFIG. 2 in accordance with an embodiment of the invention.

FIG. 4 is a schematic cross-sectional view of a microbial fuel cellcontaining a proton permeable membrane in accordance with an embodimentof the floating microbial fuel cell aerator of FIG. 2

FIG. 5 is a schematic illustration of the components of the buoyancymanagement system of FIG. 2 in accordance with an embodiment of theinvention.

FIG. 6 is a schematic view of a sediment microbial fuel cell aerator inaccordance with one embodiment of the invention.

FIG. 7 is a flowchart showing the process that can be used to convertorganic matter in sediments and pore-waters to electricity with themicrobial fuel cell aerator of FIG. 6 in accordance with an embodimentof the invention.

DETAILED DESCRIPTION

The detailed description set forth below in connection with the appendeddrawings is intended as a description of the presently preferredembodiments of a microbial fuel cell aerator provided in accordance withthe present invention and is not intended to represent the only forms inwhich the present invention may be constructed or utilized. Thedescription sets forth the features of the present invention inconnection with the illustrated embodiments. It is to be understood,however, that the same or equivalent functions and structures may beaccomplished by different embodiments that are also intended to beencompassed within the spirit and scope of the invention. As denotedelsewhere here, like element numbers are intended to indicate likeelements or features.

A microbial fuel cell (“MFC”) is an established technology at the smalllaboratory scale that is only now being scaled up to meet commercial andmunicipal requirements. This technology basically works by inserting awire into the metabolism of bacteria. As shown in FIG. 1, specificbacteria are grown on the surface of an anode. Organic rich, oxygendepleted waters are passed over the anode and the bacteria break downthe organic material through extracellular digestion. In this process,the bacteria transport electrons across their intracellular membranes todo cellular work. These special bacteria then pass the electron to theanode as a terminal electron acceptor. The anode chamber is separatedfrom a cathode chamber by a proton-permeable membrane or by anappropriate distance through the water. The anode is connected to thecathode by a wire and the electron flow through the wire provides anelectrical current. At the cathode, the electrons combine with protonsand oxygen to form pure water. Alternate electron acceptors are possibleat the cathode.

The membrane fuel cell aerator (“MFCA”) modifies an MFC to run on theorganic material in a body of water and produce electricity while alsorespiring some of that organic material to inorganic nutrients while atthe same time using the energy to further enhance gas exchange andmixing in a way that is synergistic with the performance of the MFCA.The MFC provides a renewable energy source with limited carbonemissions, and therefore a small carbon footprint. At the same time, theactivities of the MFC respire some of the organic material without usingoxygen from the water itself. By transferring the electrons to anair-cathode, in which the cathode is exposed to atmospheric oxygen, thisaquatic respiration is accomplished directly from the air rather thanfrom the oxygen dissolved in the water. This effectively reduces thebiological oxygen demand (“BOD”) of the water and is a direct substitutefor some of the energy that would have been required to aerate the waterto meet that BOD requirement. Thus, less energy is required and thebalance is supplied by a renewable source, the very organic materialwhose respiration requires oxygen. The electricity is used to mix wateror further enhance gas exchange and the choices of locations of themixing and anode feedback to enhance the effectiveness of the electronuptake on the anode of the MFC.

The microbial fuel cell based aeration approach described here creates anovel solution to the cost-effective aeration of aquaculture operationsby combining microbial fuel cells and electricity-powered aerationsystems. This combination reduces the demand for gas exchange, cleansthe water and provides a source of renewable energy for traditionalaeration in a device that can either be integrated into the pond or be afree-floating or free-standing installation. The combination is a green,cost-effective replacement for traditional aeration in many applicationswith special relevance to aquaculture.

The MFCA utilizes a renewable energy source for the energy requirementsof the aeration and gas management system. This energy source is thedissolved and fine particulate organic material in the water whoserespiration is creating an oxygen demand. This form of energy isproduced with little emission of fossil fuel carbon dioxide. Thepotential source of this energy is directly related to the amount oforganic material in the pond. As it declines, so does the requirementfor aeration. As it increases, so does the aeration demand. Thus, thedynamics of the source of energy and the requirement for it are linked.

The unique form of respiration in an MFC, accomplished by an air-cathodein this device, effectively allows some of the oxygen in the atmosphereto substitute for oxygen demand in the water. Since mixing in theatmosphere is rapid and the atmosphere has 20% oxygen content, thissource of oxygen is not the limiting factor in the MFCA process. Everyoxygen molecule used at the air-cathode is one less oxygen moleculerequired from within the water. This will reduce the demand for aerationwhen organic material processing rates are high. The amount of thisreduction in BOD is tied to the effectiveness of the air-cathode, butpreliminary calculations indicate that when enough MFCA devices arepresent to cover 100% of the BOD aeration, about 10-25% of the oxygendemand will be met by MFC conversion.

In one embodiment, the MFCA is a stand-alone device that is tethered to,or sits in, the middle of a pond or other body of water. It isself-powered by the organic material in the water. Thus, it does notrequire an additional source of electricity from the power grid. Thisreduces the infrastructure costs of providing power to the edge of everypond or water body, the risks associated with running electricity into abody of water and the maintenance of that infrastructure system.

Reducing the costs of aeration may make a variety of products andprocesses more cost-effective and bring some new technologies to market.The energy costs of aeration are a large component of intensiveaquaculture. Lower costs may improve the economics of some of the moresustainable fish farming approaches that are currently stymied by energycosts. Intensive algae farming has high costs associated with gasexchange for getting rid of oxygen and adding carbon dioxide. The MFCAcould make some of those approaches more cost effective.

The MFC is configured so that the cathode is exposed to the air and theanode is submerged in anaerobic, organic-rich waters or sediments. Incertain embodiments, the anode and cathode are separated by a protonpermeable membrane, while in others, the protons simply flow through thebody of water and the physical separation of the anode and cathode by avolume of water creates the same effect. In some embodiments, the waterfor the anode is supplied by an electric pump and may pass through oneor more pre-concentration devices to increase the concentration oforganic particles that arrive at the anode. The pumping system may alsobe configured to allow ambient bacteria and protists to remove theremainder of the dissolved oxygen before the water comes in contact withthe anode.

The MFC makes low-voltage DC. An electricity management system providesthe appropriate regulation of this current and conversion into othervoltages and/or to AC to provide power to the other components of thesystem. The electricity management system may be connected to a publicelectrical grid and/or a battery. The electricity management system isalso used to manage the data from sensors in the water, in the internalcomponents of the system or other data sensors. These sensors feed datainto the electricity management system that then control the othercomponents of the system including the speed of pumps and aerators, theactivity of pre-concentration devices, the current out to the grid,warning and alarms systems and other requirements.

The anode of the MFC requires contact with organic carbon-rich materialsin an anaerobic fluid and a carbon management system is configured toensure contact between the anode and the organic materials. In oneembodiment, this is achieved by pumping water rich in organic materialsinto an anode chamber, either directly or after passing through one ormore pre-concentration devices. In another embodiment, this is achievedby managing exposure of the anode to sediments rich in organic materialsand organic rich pore-waters.

Electricity from the MFC is used, in part, to power one or more aerationor mixing systems of a variety of designs. This is designed too aerateor mix the surrounding waters without impacting the provision ofanaerobic conditions to the anode. The aeration or mixing can beperformed by any of a variety of standard devices that enhance the gasexchange between air and water. In one embodiment, this may be a simplemotor-powered DC air pump that captures ambient air, compresses it andtransfers it to a certain depth in the water to provide bubbles of airto the pond. In another embodiment, this can be a water pump that takesin water from either the anode or the ambient environment and pushes itinto the air in small droplets, much like a fountain, or down intodeeper water to aid in mixing. In yet another embodiment, the aerationor mixing device includes a paddle wheel or brush wheel driven by a DCmotor that thrashes the surface of the water, both flinging dropletsinto the air and forcing bubbles into the water. In some embodiments,the movement of the water alone is adequate to improve gas exchange bybringing low oxygen water close to the surface.

In some embodiments, the air-cathode is maintained at the surface of thebody of water to remain in contact with the air, while the anode and/orcarbon management systems are in contact with the water or sediments. Aflotation system is designed to maintain these configurations in theface of environmental fluctuations in the body of water.

The MFCA has different embodiments depending on the specificrequirements, size, and shape of the pond or body of water in which itresides. Two embodiments, a floating microbial fuel cell aerator(“FMFCA), shown in FIGS. 2, 3, 4 and 5, and a sediment microbial fuelcell aerator (“SMFCA”), shown in FIGS. 6 and 7, are described below.

As shown in FIGS. 2, 3, 4 and 5, one embodiment of the MFCA is afloating microbial fuel cell aerator (“FMFCA”). The FMFCA 100 embodimentincludes an MFC subsystem 110, an electricity management subsystem 120,a fluid management subsystem 130, an aerator subsystem 140, and abuoyancy management subsystem 150. In one embodiment, these parts areintegrated into a single package. In one embodiment, the FMFCA 100floats on the surface of a pond or other body of water with at leastpart of the FMFCA exposed to the air. In one embodiment, the FMFCA 100is tethered into a desired location in the pond.

As shown in FIGS. 3 and 4, the MFC subsystem 110 of the FMFCA 100includes an anode chamber 112, an anode 114 and an air-cathode 118. Inone embodiment, the anode 114 and the air-cathode 118 are separated by aproton permeable membrane 116.

The anode chamber 112 is configured to contain the anode 114, and isconnected to the fluid management subsystem 130. The anode chamber 112is enclosed to keep a water-tight separation between the fluid in theanode chamber and that in the pond in which it is located.

The anode 114 may be made from any of a variety of materials, includinggraphite plates or rods, carbon fiber cloths or wires, carbon or metalaerogels or other configurations that maximize the amount of surfacearea and the ability of the organic material-rich water to flow throughthe system. The anode 114 supports bacteria that respire organicmaterial in the fluid. In one embodiment, the bacteria form a biofilm onthe surface of the anode 114. The material for the anode 114 and thebacteria are selected to accommodate the best bacteria for the selectedwaters and organic material.

As shown in FIG. 4, the proton permeable membrane 116 is located on theupper surface of the anode chamber 112 and separates the anode chamber112 and the air-cathode 118. The proton permeable membrane 116 allowsprotons to cross from the anode chamber 112 to the air-cathode 118.

In one embodiment, the proton permeable membrane 116 is coated with theair-cathode 118. The combination of the proton permeable membrane 116and air-cathode 118 is made of a material having a high surface areathat can both transfer protons and electrons and mediate the mixing ofgaseous oxygen in air, protons crossing the proton permeable membrane116 and electrons from the air-cathode 118. In one embodiment, theproton permeable membrane 116 and air cathode combination is made of amaterial selected from the group consisting of organic polymermembranes, carbon granules, fibers, aerogels, bacterial coatings andmetal coatings such as platinum and other metals.

In the FMFCA 100 shown in FIGS. 2 and 4, the MFC subsystem 110 isdesigned so that the air-cathode 118 is exposed to the air and the anodechamber 112 that holds the anode 114 is submerged in organic-rich watersbeneath the surface of a pond. In one embodiment of the device, the MFCsubsystem 110 is arranged as a flat box that is wider and longer than itis deep, to maximize the surface area of the air-cathode 118 for aspecific volume of the anode chamber 112. Other configurations where alarger anode volume is required can have any of a variety of shapes thatkeep the area of the air-cathode to an adequate size for the electronflow out into the atmosphere.

In the embodiment shown in FIGS. 2 and 3, the electricity managementsubsystem 120 includes a wire 122, a power management system 124,sensors 125, electrical grid 126, a communication device 127 and abattery 128.

The wire 122 electrically connects the anode 114 with the air-cathode118.

The embodiment shown in FIG. 3 includes the battery 128 for storingpower for later use. The battery 128 may be any suitable type ofbattery.

The communication device 127 allows the electricity management subsystem120 to interact with other devices and sensors. The communication device127 may be wired or wireless.

One or more sensors 125 collect information. In one embodiment, theelectricity management subsystem 120 includes hardware and software thatuse information collected by the sensors 125 to modify the performanceof the FMFCA 100. In some embodiments, these modifications can includechanging the speed of various motors, turning part or all of the deviceon or off, reversing the direction of flow of a pump, signalingperformance data to another device and other activities. In otherembodiments of the device, it may run on other voltages or evenalternating current.

In the embodiment shown in FIG. 3, the electricity management subsystemmay be connected to the electrical grid 126 to provide electricity tothe electrical grid 126 when the MFC subsystem 110 produces surpluselectricity, and using electricity from the electrical grid 126 whenmore electricity is required to power the FMFCA 100.

In the FMFCA 100 shown in FIGS. 2, 3 and 4, the organic carbonmanagement subsystem is the fluid management subsystem 130, whichpre-processes and transfers organic carbon-rich ambient water to theanode chamber 112. The fluid management subsystem 130 includes a pump132 that may be powered by the electricity management system 120. Incertain embodiments, the fluid management subsystem 130 includes asnorkel 134 or other tube that draws water from a specific depth andpre-concentration devices 136 that increase the concentration oforganic-rich particles in the water. In certain embodiments, the fluidmanagement subsystem 130 includes embedded sensors that can measureinternal and external conditions such as oxygen concentration, currentflow, clogging or other performance related characteristics.

In the embodiment shown in FIG. 3, the fluid management subsystem 130includes a filter or concentrator 136 to ensure that the water thatflows into the anode chamber 112 is fit to be processed by the bacteria.

In the embodiment shown in FIG. 4, the fluid management subsystem 130includes a fluid outflow 138 to remove excess fluid, such as water, fromthe anode chamber 112.

In the embodiment shown in FIGS. 2 and 3, the aerator subsystem 140includes an aerator motor 142 that drives an aeration device 144. In theembodiment shown in FIG. 2, the aeration device 144 is a brush wheel.

In one embodiment of the FMFCA 100 shown in FIG. 2, the buoyancymanagement subsystem 150 shown in FIG. 5 includes a frame 152 to holdthe other subsystems 110, 120, 130 and 140 in the best configuration,floats 154 that provide enough buoyancy to hold the FMFCA 100 at theproper water level, hand-holds 156 for moving the FMFCA 100 in and outof the water and tethers 158 that allow the FMFCA 100 to be safelytethered.

During operation of the FMFCA 100, the bacteria respire organic materialin the anode chamber 112 and produce electrons and protons. As shown inFIG. 3, the protons enter the air-cathode 118 via the proton permeablemembrane 116. The electrons are collected at the anode 114 and flowthrough the wire 122 to the air-cathode 118. Gaseous oxygen fromatmospheric air, protons crossing the proton permeable membrane 116 andelectrons from the air-cathode 118 combine at the air-cathode 118 toproduce water. The flow of electrons from the anode 114 to theair-cathode 118 produces low-voltage direct current (“DC”).

In the embodiment shown in FIG. 3, the electricity management subsystem120 converts the low-voltage DC produced by the MFC subsystem 110 into acurrent required by the fluid management subsystem 130 and/or theaerator subsystem 140. The electricity management subsystem 120 alsomanages the quality and flow of electricity and includes the powermanagement system 124 that is programmed or hardwired to ensure that theFMFCA 100 functions as intended.

In one embodiment, the electricity management subsystem 120 converts lowvoltage DC produced by the MFC subsystem 110 to 12 volts and shunts thecurrent to run a 12 volt pump 132 in the fluid management subsystem 130and/or a 12 volt motor 142 in the aerator subsystem 140. The electricitymanagement subsystem 120 also diverts a small amount of the power tocover the energy needs of the power management system 124 includingmicro-processors and switches that manage the functions of theelectricity management subsystem 120.

The SMFCA 300 shown in FIGS. 6 and 7 includes the components of an MFCsubsystem 310 including the MFC anode 314 and the MFC air-cathode 318,an electricity management subsystem 320, an organic material collectionsubsystem 330, an aerator subsystem 340 and a buoyancy managementsubsystem 350.

In the SMFCA device shown in FIGS. 6 and 7, the MFC subsystem 310 issimilar in principle to that of the MFC subsystem 110 of the FMFCA 100described above. The MFC subsystem 310 includes an anode 314 and anair-cathode 318. The MFC subsystem 310 shown in FIGS. 6 and 7 isdesigned so that the air-cathode 318 floats on the surface of the waterand is exposed to the air. The anode 314 is embedded in the sediment atthe bottom of the pond or body of water so that sediment rich in organicmaterial falls onto, covers, and surrounds the anode 314.

The anode 314 and air-cathode 318 can have a variety of designs based onthe specific application. In one embodiment, the anode 314 consists ofgraphite plates, rods, cloths, or other materials arrayed in such a wayas to maximize the surface area in close contact with the organicmaterial. This type of anode may be wrapped in wires or have wiresembedded in the conducting materials to improve electron flow. The anodewill be of any shape that maximizes the contact with organic-richsediments and pore-waters and the exchange of pore-water to retain asteady supply of new organics in contact with the anode surface. In someembodiments, the anode is designed as an integral part of a sedimentcollection system in the organic carbon management subsystem 330 thatpre-concentrates the sinking particles and focuses them around theanode. This may be a simple conical device or in more complex ponddesigns, a hydrodynamic system that has areas of high turbulence to keepmost particles suspended and strategic areas of low turbulence where theorganic particles preferentially settle. In these designs, the anodewould be arrayed in the areas of low turbulence so that the particlessettled in and around the anode.

In one embodiment, the air cathode 318 is made of a material selectedfrom the group consisting of organic polymer membranes, carbon granules,fibers, sheets, aerogels, and metal coatings such as platinum and othermetals.

The electricity management subsystem 320 includes a wire 322, a powermanagement system 324, one or more sensors 325, an electrical grid 326,a communication device 327 and a battery 328.

The wire 322 electrically connects the anode 314 with the air-cathode320, and carries electricity from the anode 314 at the bottom of thepond to the air-cathode 320 floating on the surface of the pond.

The power management system 324, sensors 325, electrical grid 326,communication device 327 and battery 328 are substantially similar tothe power management system 124, sensors 125, electrical grid 126,communication device 127 and battery 128 as described above in referenceto FMFCA 100 in FIG. 3.

As shown in FIGS. 6 and 7, the organic carbon management subsystem 330gathers sediment containing organic material from a large area so thatit will come into contact with the anode 314. Because the anode 314 isembedded in the sediment and must be covered and surrounded by organicmaterial, it is necessary that as much organic material as possiblesettle on the anode 314. In the embodiment shown in FIGS. 6 and 7, theorganic carbon management subsystem 330 includes a settling tray 332,which consists of a large, gently sloping surface that operates muchlike a funnel to direct falling organic material towards the anode 314.The settling tray 332 may be made of any suitable material. In oneembodiment, the settling tray is made of plastic. In another embodiment,the organic carbon management subsystem 330 includes pumps and tubesthat suck in organic material from other areas of the pond and deliverthe organic material to the anode 314. In one embodiment, the organiccarbon management subsystem 330 is unnecessary when the anode 314 islocated where organic material naturally, or by engineered design,collects in a certain area of the pond or body of water.

In the embodiment shown in FIG. 6, the buoyancy management subsystem 350is largely the same as the buoyancy management subsystem 150 illustratedin FIG. 5. It includes a frame 152 to hold the other subsystems 310,320, 330 and 340 in the best configuration, floats 154 that provideenough buoyancy to hold the SMFCA 300 at the proper water level,hand-holds 156 for moving the SMFCA 300 in and out of the water andtethers 158 that connect to the anode 314.

During operation of the SMFCA 300, the bacteria respire organic materialat the anode 314 and produce electrons and protons. As shown in FIG. 7,the protons flow through the water to the air-cathode 318. Because thesediment at the anode 314 and the air at the air-cathode 318 exchangewater slowly, no proton permeable membrane is required. The electronsare collected at the anode 314 and flow through the wire 322 to theair-cathode 318. Gaseous oxygen from atmospheric air, protons flowingthrough the water and electrons from the air-cathode 318 combine at theair-cathode 318 to produce water. The flow of electrons from the anode314 to the air-cathode 318 produces low-voltage direct current (“DC”).

Although limited embodiments of the MFCA have been specificallydescribed and illustrated herein, many modifications and variations willbe apparent to those skilled in the art. Accordingly, it is to beunderstood that the MFCA constructed according to principles of thisinvention may be embodied other than as specifically described herein.The invention is also defined in the following claims.

What is claimed is:
 1. A device for mixing and aerating a body of waterfor growing an organism, the device comprising: a microbial fuel cellcomprising an anode and a cathode; an electricity management subsystemelectrically connecting the anode and the cathode; and a mixingsubsystem electrically connected to the electricity managementsubsystem.
 2. The device according to claim 1, wherein the mixingsubsystem comprises an apparatus selected from the group consisting ofair pumps, water pumps, paddle wheels, brush wheels and combinationsthereof.
 3. The device according to claim 1, wherein the mixingsubsystem comprises an aerating apparatus or a mixing apparatus.
 4. Thedevice according to claim 1, further comprising an organic materialmanagement subsystem.
 5. The device according to claim 4, wherein theorganic material management subsystem comprises a pump andpre-concentration devices
 6. The device according to claim 4, whereinthe organic material management subsystem comprises a settling tray. 7.The device according to claim 1, further comprising a buoyancymanagement subsystem.
 8. The device according to claim 1, wherein thecathode is exposed to air.
 9. The device according to claim 1, whereinthe microbial fuel cell further comprises a proton permeable membrane.10. A method for mixing a body of water for growing an organism using adevice, the device comprising: a microbial fuel cell comprising an anodeand a cathode, an electricity management subsystem electricallyconnecting the anode and the cathode, and a mixing subsystemelectrically connected to the electricity management subsystem; themethod comprising: providing bacteria to the anode, providing organicmaterial to the bacteria at the anode, allowing the bacteria to produceelectrons at the anode, and powering the mixing subsystem withelectricity flowing from the anode to the cathode through theelectricity management subsystem.
 11. The method of claim 10, whereinthe organic material is provided by the body of water.